WO2006036241A2 - Nitrided bipolar plates - Google Patents

Nitrided bipolar plates Download PDF

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Publication number
WO2006036241A2
WO2006036241A2 PCT/US2005/023130 US2005023130W WO2006036241A2 WO 2006036241 A2 WO2006036241 A2 WO 2006036241A2 US 2005023130 W US2005023130 W US 2005023130W WO 2006036241 A2 WO2006036241 A2 WO 2006036241A2
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WO
WIPO (PCT)
Prior art keywords
electrochemical conversion
bipolar plates
bipolar
conversion assembly
nitrided
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2005/023130
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French (fr)
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WO2006036241A3 (en
Inventor
Michael K. Budinski
Gayatri Vyas
Augusto O. Kunrath
John J. Moore
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Motors Liquidation Co
Original Assignee
General Motors Corp
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Filing date
Publication date
Application filed by General Motors Corp filed Critical General Motors Corp
Priority to JP2007532314A priority Critical patent/JP4814243B2/en
Priority to DE112005002235.8T priority patent/DE112005002235B4/en
Publication of WO2006036241A2 publication Critical patent/WO2006036241A2/en
Anticipated expiration legal-status Critical
Publication of WO2006036241A3 publication Critical patent/WO2006036241A3/en
Ceased legal-status Critical Current

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Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H01M8/0206—Metals or alloys
    • H01M8/0208—Alloys
    • H01M8/021—Alloys based on iron
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H01M8/0223—Composites
    • H01M8/0228—Composites in the form of layered or coated products
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M2008/1095—Fuel cells with polymeric electrolytes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
    • H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • H01M8/0263—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant having meandering or serpentine paths
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • H01M8/0265—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant the reactant or coolant channels having varying cross sections
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49345—Catalytic device making

Definitions

  • the present invention relates to electrochemical conversion cells, commonly referred to as fuel cells, which produce electrical energy by processing first and second reactants, e.g., through oxidation and reduction of hydrogen and oxygen.
  • a typical cell comprises a polymer membrane (e.g., a proton exchange membrane)- that is positioned between a pair of gas diffusion media layers and catalyst layers.
  • a cathode plate and an anode plate are positioned at the outermost sides adjacent the gas diffusion media layers, and the preceding components are tightly compressed to form the cell unit.
  • the voltage provided by a single cell unit is typically too small for useful application. Accordingly, a plurality of cells are typically arranged and connected consecutively in a "stack" to increase the electrical output of the electrochemical conversion assembly or fuel cell.
  • two adjacent cell units can share a common polar plate, which serves as the anode and the cathode for the two adjacent cell units it connects in series.
  • a plate is commonly referred to as a bipolar plate and typically includes a flow field defined therein to enhance the delivery of reactants and coolant to the associated cells.
  • Bipolar plates for fuel cells are typically required to be electrochemically stable, electrically conductive, and inexpensive.
  • Metallic bipolar plates are advantageous because they can be made very thin (e.g., ⁇ 0.25mm) and can be formed into a final shape by inexpensive metal forming techniques, such as stamping.
  • metal plates are susceptible to corrosion.
  • An active corrosion process in a fuel cell stack can increase the membrane resistance and the contact resistance of the bipolar plates, reducing the power density of the stack.
  • Stainless steels have been considered for use in forming bipolar plates, due primarily to their inherent corrosion resistance and the relatively inexpensive material cost. Accordingly, the present inventors have recognized a need to provide for improved schemes for enabling the use of Stainless steels in forming bipolar plates. BRIEF SUMMARY OF THE INVENTION
  • an electrochemical conversion assembly comprising a plurality of electrochemical conversion cells, and a plurality of electrically conductive bipolar plates.
  • the electrochemical conversion cells are configured to communicate with first and second reactant supplies. Adjacent ones of the electrochemical conversion cells are separated by respective ones of the plurality of bipolar plates.
  • the bipolar plates comprise an alloy comprising Fe and Cr.
  • a surface portion of the bipolar plates comprises a single phase nitrided structure. The single phase nitrided structure of the bipolar plates is in contact with portions of the electrochemical conversion cells.
  • a method of fabricating an electrochemical conversion assembly comprising a plurality of electrochemical conversion cells and a plurality of electrically conductive bipolar plates.
  • Bipolar plates are formed from an alloy comprising Fe and Cr.
  • a plasma nitriding process is utilized to create a single phase nitrided structure along a surface portion of respective ones of the bipolar plates.
  • Adjacent ones of the electrochemical conversion cells are positioned such that they are separated by respective ones of the plurality of bipolar plates and such that the single phase nitrided structure of the bipolar plates is in contact with portions of the electrochemical conversion cells.
  • FIG. 1 is an illustration of a bipolar plate according to one embodiment of the present invention
  • FIG. 2 is a cross-sectional illustration of a nitrided portion of a bipolar plate according to one embodiment of the present invention
  • FIG. 3 is a schematic illustration of an electrochemical conversion assembly according to one embodiment of the present invention.
  • FIG. 4 is a schematic illustration of a vehicle having a fuel processing system and an electrochemical conversion assembly according to one embodiment of the present invention.
  • the electrochemical conversion assembly 10 comprises a plurality of electrochemical conversion cells 20 and a plurality of electrically conductive bipolar plates 30.
  • a variety of conversion assembly configurations are contemplated by the present invention, as long as the assembly utilizes one or more bipolar plates 30 between some or all of the respective electrochemical conversion cells 20.
  • the specific structure of the conversion assembly 10 and the individual conversion cells 20 is beyond the scope of the present invention and may be gleaned from any existing or yet to be developed teachings related to the design of an assembly that is capable of generating electricity from first and second chemical reactant supplies Ri, R 2 in communication with the electrochemical conversion cells 20.
  • One or more reactant outlets R OUT are also typically provided.
  • a bipolar plate 30 according to the present invention may comprise a flowfield portion 32 and fluid header portions 34 coupled to the flowfield portion 32.
  • the flowfield portion 32 can include flowfield channels 35 defined between opposite, electrically conductive sides 36, 38 of the bipolar plate 30.
  • adjacent electrochemical conversion cells 20 are separated by respective ones of the plurality of bipolar plates 30.
  • the bipolar plates 30 comprise an alloy of Fe and Cr and include a surface portion that comprises a single phase nitrided structure. Specifically, referring to Fig.
  • the illustrated single phase nitrided structure defines respective nitrided layers 46, 48 along opposite sides 36, 38 of the bipolar plate 30.
  • the nitrided layers 46, 48 defined on opposite sides of a selected bipolar plate 30 can be placed in electrical contact with a corresponding electrochemical conversion cell 10 in the conversion assembly 10.
  • the bipolar plates 30 will contact the gas diffusion media layers of the electrochemical conversion cell 10.
  • the single phase nitrided structure may. be produced by any suitable fabrication process. It is believed that this is achieved by forming a homogenous and adherent single-phase layer known as expanded austenite. This single-phase layer is also referred to in the literature as a gamma N, S or m phase. Temperatures above 400°C normally result in the formation of mixed phases, which perform poorly as they are more likely to exhibit significant corrosion. The formation of CrN precipitates, for instance, normally leads to the deterioration of both pitting corrosion resistance and homogenous corrosion resistance.
  • One fabrication process that yielda the expanded austenite phase and has achieved high corrosion resistance without significant sacrifice to the mechanical and electrical properties of the alloy comprises a plasma nitriding process.
  • a plasma nitriding process it is often advantageous to maintain the temperature of the bipolar plates at about 375°C or above about 350°C and below about 400°C.
  • the temperature of a bipolar plate being processed can be monitored by utilizing, a thermocouple secured to the plate during processing. Where the thickness or some other aspect of the plate does not permit effective use of a thermocouple, the temperature of the bipolar plate can be monitored by monitoring the temperature of a dummy plate configured to mimic the thermodynamic properties of the bipolar plate.
  • At least one class of suitable plasma nitriding processes is characterized by a pressure of between about 0.5 Torr and about 5.0 Torr, and a bias voltage of between about 35QV and about 650V.
  • Other embodiments are characterized by a pressure of between about 1.5 Torr and about 2.0 Torr, and a bias voltage of between about 580V and about 630V.
  • the impedance of the plasma is dependent on the gas composition and pressure. Accordingly, the suitability of particular voltage values will often be a function of gas composition and pressure.
  • those practicing the present invention should be aware that if one uses a secondary heat source, the electric parameters controlling the plasma could be varied independently of temperature of the part. In this manner, the present invention may be practiced at relatively lower "voltage and current in the plasma by partially heating the part with a suitable supplemental heating element.
  • the plasma nitriding process can be characterized by the utilization of a process gas comprising N 2 and H 2 .
  • a process gas composition of about 20% N 2 and about 80% H 2 , by weight.
  • Typical nitriding durations in this context extend for about 4 hours. It is noted that nitriding is a diffusion controlled process and that the thickness of the nitrided layer depends on the diffusing species, diffusing medium, diffusion temperature, duration of diffusion, and type of diffusion process (salt bath, gas, diode plasma, ion implantation, etc.). For example, the subject matter of Fig.
  • a bipolar plate 30 is characterized by a thickness of between about lOO ⁇ m and about 500 ⁇ m
  • the single phase nitrided structure defines a thickness of between about 0.001 ⁇ m and about 25 ⁇ m.
  • Suitable alloys may be selected from a variety of materials including, but not limited to, alloys comprising Ni, Mo, Mn, Si, C, or N, in combination with Fe and Cr, stainless steels, austenitic stainless steels, etc.
  • the specific structure of the conversion assembly 10 and the individual conversion cells 20, is beyond the scope of the present invention.
  • typical conversion assemblies comprise respective membrane electrode assemblies that are configured to operate with hydrogenous gas and air as the respective reactant supplies.
  • the electrochemical conversion cells 20 may comprise respective electrolytic membranes, gaseous diffusion layers, catalytic components, carbonaceous components, electrically conductive components, and combinations thereof.
  • the bipolar plates 30 illustrated in Figs. 1 and 2 comprise a flowfield defined between the opposite, electrically conductive sides of the bipolar plate 30, it is contemplated that suitable bipolar plate configurations need not include a flowf ⁇ eld.
  • a device may comprise a vehicle 100 and an electrochemical conversion assembly 110 according to the present invention.
  • the vehicle 100 may also have a fuel processing system or fuel source 120 configured to supply the electrochemical conversion assembly 110 with fuel.
  • the present invention is not limited to any specific reactant compositions, it will be appreciated by those practicing the present invention and generally familiar with fuel cell technology that the first reactant supply R 1 typically comprises oxygen and nitrogen while the second reactant supply R 2 comprises hydrogen.
  • a “device” is utilized herein to represent a combination of components and individual components, regardless of whether the components are combined with other components.
  • a “device” according to the present invention may comprise an electrochemical conversion assembly or fuel cell, a vehicle incorporating an electrochemical conversion assembly according to the present invention, etc.

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  • Engineering & Computer Science (AREA)
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Abstract

Nitrided bipolar plates and a scheme for their fabrication are provided. The present invention also contemplates device incorporating bipolar plates according to the present invention. For example, in accordance with one embodiment of the present invention, an electrochemical conversion assembly is provided. The electrochemical conversion cells of the assembly are separated by respective bipolar plates comprising an alloy of Fe and Cr. A surface portion of the bipolar plates comprises a single phase nitrided structure. According to another embodiment of the present invention, a plasma nitriding process is utilized to create a single phase nitrided structure along a surface portion of respective ones of said bipolar plates.

Description

NITRIDED BIPOLAR PLATES
BACKGROUND OF THE INVENTION
[0001] The present invention relates to electrochemical conversion cells, commonly referred to as fuel cells, which produce electrical energy by processing first and second reactants, e.g., through oxidation and reduction of hydrogen and oxygen. By way of illustration and not limitation, a typical cell comprises a polymer membrane (e.g., a proton exchange membrane)- that is positioned between a pair of gas diffusion media layers and catalyst layers. A cathode plate and an anode plate are positioned at the outermost sides adjacent the gas diffusion media layers, and the preceding components are tightly compressed to form the cell unit.
[0002] The voltage provided by a single cell unit is typically too small for useful application. Accordingly, a plurality of cells are typically arranged and connected consecutively in a "stack" to increase the electrical output of the electrochemical conversion assembly or fuel cell. In this arrangement, two adjacent cell units can share a common polar plate, which serves as the anode and the cathode for the two adjacent cell units it connects in series. Such a plate is commonly referred to as a bipolar plate and typically includes a flow field defined therein to enhance the delivery of reactants and coolant to the associated cells.
[0003] Bipolar plates for fuel cells are typically required to be electrochemically stable, electrically conductive, and inexpensive. Metallic bipolar plates are advantageous because they can be made very thin (e.g., <0.25mm) and can be formed into a final shape by inexpensive metal forming techniques, such as stamping. However, metal plates are susceptible to corrosion. An active corrosion process in a fuel cell stack can increase the membrane resistance and the contact resistance of the bipolar plates, reducing the power density of the stack. Stainless steels have been considered for use in forming bipolar plates, due primarily to their inherent corrosion resistance and the relatively inexpensive material cost. Accordingly, the present inventors have recognized a need to provide for improved schemes for enabling the use of Stainless steels in forming bipolar plates. BRIEF SUMMARY OF THE INVENTION
[0004] According to the present invention, nitrided bipolar plates and a scheme for their fabrication are provided. The present invention also contemplates device incorporating bipolar plates according to the present invention. For example, in accordance with one embodiment of the present invention, an electrochemical conversion assembly is provided comprising a plurality of electrochemical conversion cells, and a plurality of electrically conductive bipolar plates. The electrochemical conversion cells are configured to communicate with first and second reactant supplies. Adjacent ones of the electrochemical conversion cells are separated by respective ones of the plurality of bipolar plates. The bipolar plates comprise an alloy comprising Fe and Cr. A surface portion of the bipolar plates comprises a single phase nitrided structure. The single phase nitrided structure of the bipolar plates is in contact with portions of the electrochemical conversion cells.
[0005] In accordance with another embodiment of the present invention, a method of fabricating an electrochemical conversion assembly comprising a plurality of electrochemical conversion cells and a plurality of electrically conductive bipolar plates is provided. Bipolar plates are formed from an alloy comprising Fe and Cr. A plasma nitriding process is utilized to create a single phase nitrided structure along a surface portion of respective ones of the bipolar plates. Adjacent ones of the electrochemical conversion cells are positioned such that they are separated by respective ones of the plurality of bipolar plates and such that the single phase nitrided structure of the bipolar plates is in contact with portions of the electrochemical conversion cells.
[0006] Accordingly, it is an object of the present invention to provide nitrided bipolar plates and a scheme for their fabrication. Other objects of the present invention will be apparent in light of the description of the invention embodied herein.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS [0007] The following detailed description of specific embodiments of the present invention can be best understood when read in conjunction with the following drawings, where like structure is indicated with like reference numerals, where various components of the drawings are not necessarily illustrated to scale, and in which: [0008] Fig. 1 is an illustration of a bipolar plate according to one embodiment of the present invention;
[0009] Fig. 2 is a cross-sectional illustration of a nitrided portion of a bipolar plate according to one embodiment of the present invention;
[0010] Fig. 3 is a schematic illustration of an electrochemical conversion assembly according to one embodiment of the present invention; and
[0011] Fig. 4 is a schematic illustration of a vehicle having a fuel processing system and an electrochemical conversion assembly according to one embodiment of the present invention.
DETAILED DESCRIPTION
[0012] Referring to Figs. 1-3, an electrochemical conversion assembly 10 according to the present invention is illustrated. Generally, the electrochemical conversion assembly 10 comprises a plurality of electrochemical conversion cells 20 and a plurality of electrically conductive bipolar plates 30. A variety of conversion assembly configurations are contemplated by the present invention, as long as the assembly utilizes one or more bipolar plates 30 between some or all of the respective electrochemical conversion cells 20. Indeed, the specific structure of the conversion assembly 10 and the individual conversion cells 20, is beyond the scope of the present invention and may be gleaned from any existing or yet to be developed teachings related to the design of an assembly that is capable of generating electricity from first and second chemical reactant supplies Ri, R2 in communication with the electrochemical conversion cells 20. One or more reactant outlets ROUT are also typically provided.
[0013] Many aspects of the specific configuration of the bipolar plates 30 according to the present invention are also beyond the scope of the present invention. For example, referring specifically to Fig. 1, a bipolar plate 30 according to the present invention may comprise a flowfield portion 32 and fluid header portions 34 coupled to the flowfield portion 32. As is illustrated in Fig. 2, the flowfield portion 32 can include flowfield channels 35 defined between opposite, electrically conductive sides 36, 38 of the bipolar plate 30. [0014] As is illustrated in Fig. 3, adjacent electrochemical conversion cells 20 are separated by respective ones of the plurality of bipolar plates 30. The bipolar plates 30 comprise an alloy of Fe and Cr and include a surface portion that comprises a single phase nitrided structure. Specifically, referring to Fig. 2, the illustrated single phase nitrided structure defines respective nitrided layers 46, 48 along opposite sides 36, 38 of the bipolar plate 30. In this manner, the nitrided layers 46, 48 defined on opposite sides of a selected bipolar plate 30 can be placed in electrical contact with a corresponding electrochemical conversion cell 10 in the conversion assembly 10. Typically, the bipolar plates 30 will contact the gas diffusion media layers of the electrochemical conversion cell 10.
[0015] The single phase nitrided structure may. be produced by any suitable fabrication process. It is believed that this is achieved by forming a homogenous and adherent single-phase layer known as expanded austenite. This single-phase layer is also referred to in the literature as a gamma N, S or m phase. Temperatures above 400°C normally result in the formation of mixed phases, which perform poorly as they are more likely to exhibit significant corrosion. The formation of CrN precipitates, for instance, normally leads to the deterioration of both pitting corrosion resistance and homogenous corrosion resistance.
[0016] One fabrication process that yielda the expanded austenite phase and has achieved high corrosion resistance without significant sacrifice to the mechanical and electrical properties of the alloy comprises a plasma nitriding process. During nitriding, it is often advantageous to maintain the temperature of the bipolar plates at about 375°C or above about 350°C and below about 400°C. The temperature of a bipolar plate being processed can be monitored by utilizing, a thermocouple secured to the plate during processing. Where the thickness or some other aspect of the plate does not permit effective use of a thermocouple, the temperature of the bipolar plate can be monitored by monitoring the temperature of a dummy plate configured to mimic the thermodynamic properties of the bipolar plate.
[0017] At least one class of suitable plasma nitriding processes is characterized by a pressure of between about 0.5 Torr and about 5.0 Torr, and a bias voltage of between about 35QV and about 650V. Other embodiments are characterized by a pressure of between about 1.5 Torr and about 2.0 Torr, and a bias voltage of between about 580V and about 630V. In many instances, the impedance of the plasma is dependent on the gas composition and pressure. Accordingly, the suitability of particular voltage values will often be a function of gas composition and pressure. Further, those practicing the present invention should be aware that if one uses a secondary heat source, the electric parameters controlling the plasma could be varied independently of temperature of the part. In this manner, the present invention may be practiced at relatively lower "voltage and current in the plasma by partially heating the part with a suitable supplemental heating element.
[0018] The plasma nitriding process can be characterized by the utilization of a process gas comprising N2 and H2. Specific embodiment of the present invention employ a process gas composition of about 20% N2 and about 80% H2, by weight. Typical nitriding durations in this context extend for about 4 hours. It is noted that nitriding is a diffusion controlled process and that the thickness of the nitrided layer depends on the diffusing species, diffusing medium, diffusion temperature, duration of diffusion, and type of diffusion process (salt bath, gas, diode plasma, ion implantation, etc.). For example, the subject matter of Fig. 2 is not necessarily illustrated to scale and it is contemplated that, where a bipolar plate 30 is characterized by a thickness of between about lOOμm and about 500μm, the single phase nitrided structure defines a thickness of between about 0.001 μm and about 25μm.
[0019] Suitable alloys may be selected from a variety of materials including, but not limited to, alloys comprising Ni, Mo, Mn, Si, C, or N, in combination with Fe and Cr, stainless steels, austenitic stainless steels, etc.
[0020] As is noted above, the specific structure of the conversion assembly 10 and the individual conversion cells 20, is beyond the scope of the present invention. However, it is noted that typical conversion assemblies comprise respective membrane electrode assemblies that are configured to operate with hydrogenous gas and air as the respective reactant supplies. Again by way of illustration and not limitation, the electrochemical conversion cells 20 may comprise respective electrolytic membranes, gaseous diffusion layers, catalytic components, carbonaceous components, electrically conductive components, and combinations thereof. Finally, although the bipolar plates 30 illustrated in Figs. 1 and 2 comprise a flowfield defined between the opposite, electrically conductive sides of the bipolar plate 30, it is contemplated that suitable bipolar plate configurations need not include a flowfϊeld.
[0021] Referring to Fig. 4, a device according to the present invention may comprise a vehicle 100 and an electrochemical conversion assembly 110 according to the present invention. The electrochemical conversion assembly 110-can be configured to at least partially provide the vehicle 100 with motive power. The vehicle 100 may also have a fuel processing system or fuel source 120 configured to supply the electrochemical conversion assembly 110 with fuel.
[0022] Although, the present invention is not limited to any specific reactant compositions, it will be appreciated by those practicing the present invention and generally familiar with fuel cell technology that the first reactant supply R1 typically comprises oxygen and nitrogen while the second reactant supply R2 comprises hydrogen.
[0023] It is noted that terms like "preferably," "commonly," and "typically" are not utilized herein to limit the scope of the claimed invention or to imply that certain features are critical, essential, or even important to the structure or function of the claimed invention. Rather, these terms are merely intended to highlight alternative or additional features that may or may not be utilized in a particular embodiment of the present invention.
[0024] For the purposes of describing and defining the present invention it is noted that the term "device" is utilized herein to represent a combination of components and individual components, regardless of whether the components are combined with other components. For example, a "device" according to the present invention may comprise an electrochemical conversion assembly or fuel cell, a vehicle incorporating an electrochemical conversion assembly according to the present invention, etc.
[0025} For the purposes of describing and defining the present invention it is noted that the term "substantially" is utilized herein to represent the inherent degree of uncertainty that may be attributed to any quantitative comparison, value, measurement, or other representation. The term "substantially" is also utilized herein to represent the degree by which a quantitative representation may vary from a stated reference without resulting in a change in the basic function of the subject matter at issue. [0026] Having described the invention in detail and by reference to specific embodiments thereof, it will be apparent that modifications and variations are possible without departing from the scope of the invention defined in the appended claims. More specifically, although some aspects of the present invention are identified herein as preferred or particularly advantageous, it is contemplated that the present invention is not necessarily limited to these preferred aspects of the invention.

Claims

1. A device comprising an electrochemical conversion assembly, said electrochemical conversion assembly comprising a plurality of electrochemical conversion cells and a plurality of electrically conductive bipolar plates, wherein: said electrochemical conversion cells are configured to communicate with first and second reactant supplies; adjacent ones of said electrochemical conversion cells are separated by respective ones of said plurality of bipolar plates; said bipolar plates comprise an alloy comprising Fe and Cr; a surface portion of said bipolar plates comprises a single phase nitrided structure; and said single phase nitrided structure of said bipolar plates is in contact with portions of said electrochemical conversion cells.
2. A device as claimed in claim 1 wherein said single phase nitrided structure comprises expanded austenite.
3. A device as claimed in claim 1 wherein said single phase nitrided structure defines a nitrided layer along said surface portion of said bipolar plate.
4. A device as claimed in claim 1 wherein said single phase nitrided structure defines respective nitrided layers along opposite sides of said bipolar plates such that respective nitrided layers defined on opposite sides of a selected bipolar plate contact one of a pair of electrochemical conversion cells separated by said selected bipolar plate.
5. A device as claimed in claim 1 wherein said single phase nitrided structure defines a thickness of between about 0.5μm and about 6.0μm.
6. A device as claimed in claim 1 wherein said alloy further comprises Ni, Mo, Mn, Si, C, N and combinations thereof.
7. A device as claimed in claim 1 wherein said alloy comprises Fe, Cr, Ni, Mn, Si, and C.
8. A device as claimed in claim 1 wherein said alloy comprises an austenitic stainless steel.
9. A device as claimed in claim 1 wherein said first reactant supply comprises a source of hydrogenous gas and said second reactant supply comprises a source of air.
10. A device as claimed in claim 1 wherein said bipolar plates comprise a flowfield defined between opposite, electrically conductive sides of said bipolar plate.
11. A device as claimed in claim 1 wherein said electrochemical conversion cells comprise respective membrane electrode assemblies.
12. A device as claimed in claim 1 wherein said electrochemical conversion cells comprise respective electrolytic membranes, gaseous diffusion layers, catalytic components, carbonaceous components, electrically conductive components, and combinations thereof.
13. A device as claimed in claim 1 wherein said device further comprises a fuel processing system or fuel source for providing a hydrogenous gas to said electrochemical conversion assembly.
14. A device as claimed in claim 1 wherein: said device further comprises a vehicle; and said electrochemical conversion assembly is configured to at least partially provide said vehicle with motive power.
15. A device comprising an electrochemical conversion assembly, said electrochemical conversion assembly comprising a plurality of electrochemical conversion cells and a plurality of electrically conductive bipolar plates, wherein: said electrochemical conversion cells comprise respective membrane electrode assemblies and are configured to communicate with first and second reactant supplies; said first reactant supply comprises a source of hydrogenous gas; said second reactant supply comprises a source of air; adjacent ones of said electrochemical conversion cells are separated by respective ones of said plurality of bipolar plates; said bipolar plates comprise an alloy comprising Fe, Cr, Ni, Mn, Si, and C; said bipolar plates comprise a flowfϊeld defined between opposite, electrically conductive sides of said bipolar plate; a surface portion of said bipolar plates comprises a single phase nitrided structure comprising expanded austenite and defining respective nitrided layers along opposite sides of said bipolar plates such that respective nitrided layers defined on opposite sides of a selected bipolar plate contact one of a pair of electrochemical conversion cells separated by said selected bipolar plate.
16. A method of fabricating an electrochemical conversion assembly comprising a plurality of electrochemical conversion cells and a plurality of electrically conductive bipolar plates, said method comprising: providing a plurality of bipolar platea formed from an alloy comprising Fe and Cr; utilizing a plasma nitriding process to create a single phase nitrided structure along a surface portion of respective ones of said bipolar plates; and positioning adjacent ones of said electrochemical conversion cells such that they are separated by respective ones of said plurality of bipolar plates and such that said single phase nitrided structure of said bipolar plates is in contact with portions of said electrochemical conversion cells.
17. A method of fabricating, an electrochemical conversion assembly as claimed in claim 19 wherein a temperature of said bipolar plates is maintained above about 350°C and below about 400°C during said plasma nitriding process.
18. A method of fabricating an electrochemical conversion assembly as claimed in claim 19 wherein a temperature of said bipolar plates is maintained at about 375 °C during said plasma nitriding process.
19. A method of fabricating an electrochemical conversion assembly as claimed in claim 19 wherein a temperature of said bipolar plates is monitored by utilizing a thermocouple secured to said plate.
20. A method of fabricating an electrochemical conversion assembly as claimed in claim 19 wherein a temperature of said bipolar plates is monitored by monitoring the temperature of a dummy plate configured to mimic the thermodynamic properties of respective ones of said bipolar plates.
21. A method of fabricating an electrochemical conversion assembly as claimed in claim 19 wherein said plasma nitriding process is characterized by a pressure of between about 0.5 Torr and about 5.0 Torr.
22. A method of fabricating an electrochemical conversion assembly as claimed in claim 19 wherein said plasma nitriding process is characterized by a bias voltage of between about 35OV and about 650V.
23. A method of fabricating an electrochemical conversion assembly as claimed in claim 19 wherein said plasma nitriding process is characterized by the utilization of a process gas comprising N2 and H2.
24. A method of fabricating an electrochemical conversion assembly as claimed in claim 26 wherein said process gas comprises about 20% N2 and about 80% H2, by weight.
PCT/US2005/023130 2004-09-16 2005-06-30 Nitrided bipolar plates Ceased WO2006036241A2 (en)

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JP2008513952A (en) 2008-05-01
US20060053627A1 (en) 2006-03-16

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